Carrier for supporting textile material in a wet treatment machine
    7.
    发明授权
    Carrier for supporting textile material in a wet treatment machine 失效
    用于在湿式处理机中支撑纺织材料的载体

    公开(公告)号:US5444997A

    公开(公告)日:1995-08-29

    申请号:US218573

    申请日:1994-03-28

    IPC分类号: D06B5/16 D06B23/04 D06B5/18

    CPC分类号: D06B5/16 D06B23/04

    摘要: Textile yarn package supporting carriers are disclosed for use in textile dyeing machines to enable the machine to be effectively operated at less than full capacity. Each carrier has a base with multiple upstanding package supporting posts equipped with interchangeable adapters to accommodate differing numbers of yarn packages up to the maximum capacity of the carrier. An upstanding wall on the base defines an enclosure for retaining treating liquid, and the wall has a selectively movable and removable panel for forming a liquid weir at a selectively variable level relative to the base to determine a maximum level of liquid which may be retained in the carrier enclosure.

    摘要翻译: 公开了纺织纱线包装支撑载体用于纺织染色机,以使机器能够以小于满容量有效地操作。 每个承运人具有多个直立的包装支撑柱的基座,其具有可互换的适配器,以适应不同数量的纱线包装,直到载体的最大容量。 底座上的一个直立的壁限定一个用于保持处理液体的外壳,并且该壁具有一个选择性可移动的和可拆卸的面板,用于以相对于底座的选择性可变的水平形成一个液体堰,以确定可保留在 载体外壳。

    Process for the production of butane-1,4-diol
    9.
    发明授权
    Process for the production of butane-1,4-diol 失效
    制备丁烷-1,4-二醇的方法

    公开(公告)号:US4584419A

    公开(公告)日:1986-04-22

    申请号:US673797

    申请日:1984-11-21

    摘要: A process for the production of butane-1,4-diol comprises hydrogenating a di(C.sub.1 to C.sub.3 alkyl) ester of a C.sub.4 dicarboxylic acid, e.g. an ester of a but-2-en-1,4-dioic acid, such as diethyl maleate, in the vapor phase at a temperature of from about 150.degree. C. to about 240.degree. C. and at a pressure in the range of from about 25 bar to about 75 bar in the presence of a reduced copper chromite catalyst, and recovering resulting butane-1,4-diol containing reaction product. The catalyst contains, before reduction, from about 25 to about 45% by weight of copper and from about 20 to about 35% by weight of chromium and preferably has an internal surface area of at least about 30 sq. m. per gram. The process is preferably conducted in two or more reaction zones, which are preferably operated adiabatically, the feed temperature to the first zone being higher than that to at least one subsequent reaction zone.

    摘要翻译: 制备丁烷-1,4-二醇的方法包括使C4二羧酸的二(C1-C3烷基)酯例如氢化。 异丁烯-1,4-二酸如马来酸二乙酯的酯在气相中在约150℃至约240℃的温度和在 在还原的亚铬酸铜催化剂存在下,从约25巴至约75巴,并回收得到的含丁烷-1,4-二醇的反应产物。 催化剂在还原前含有约25至约45重量%的铜和约20至约35重量%的铬,优选具有至少约30平方米的内表面积。 每克。 该方法优选在两个或更多个反应区中进行,优选以绝热方式操作,第一区的进料温度高于至少一个后续反应区的进料温度。